The use of stillage in a saccharification/fermentation process of lignocellulosic biomasses, regardless of the form of the biomasses and regardless of the use of the obtained final hydrolyzed broth. The beneficial effect conferred by the stillage to the saccharification process of lignocellulosic biomasses presents among other characteristics the ability to buffer the reaction medium, especially when such process takes place in an enzymatic route, but not limited to it, regardless of the type of biomass being used and the type of pretreatment to which the biomass is subjected. Fermentation processes, such as the ethanol production, using stillage as source of nutrients such as, for example, nitrogen, for growing microorganisms, but not limited to it.
|
1. An enzymatic hydrolysis process comprising adding stillage as a buffering agent to a reaction medium containing lignocellulosic vegetal biomass, wherein said lignocellulosic vegetal biomass is selected from the group consisting of sugar cane bagasse, sugar cane straw, and a mixture of sugar cane bagasse and sugar cane straw, wherein the stillage is added in an amount that varies, in mass percentage (% w/w), from 30% to 60% and the amount of water varies, in mass percentage (% w/w), from 70% to 40%, and wherein a ph range from 4.5 to 5.5 is maintained.
2. The process according to
3. The process according to
|
|||||||||||||||||||||||||||||||||
The present invention relates to the use of stillage on saccharification/fermentation process of lignocellulosic biomasses, regardless of the form in which they present themselves and regardless of the destination given to the obtained final hydrolyzed broth. More specifically, the present invention describes the beneficial effect conferred by the stillage to the saccharification process of lignocellulosic biomasses, since it presents among other characteristics the ability to buffer the reaction medium, especially when such process takes place on enzymatic route, but not limited to it, regardless of the type of biomass being used and the type of pretreatment to which the biomass is subjected.
The present invention also relates to fermentation processes, such as the ethanol production, comprising the use of stillage as source of nutrients such as, for example, the nitrogen (N), for growing microorganisms, but not limited to it.
The present invention is in the chemical engineering area.
The enzymatic hydrolysis process, especially the saccharification of lignocellulosic biomasses, takes place in general in buffered media or under controlled pH. Thus, it is common to use buffering solutions, such as for example, sodium citrate and sodium acetate, among others, or pH control solutions such as acids and bases (e.g. sodium hydroxide, hydrochloric acid, phosphoric acid and etc) so as to maintain the pH in an ideal value in which the saccharification process of these biomasses is favored. In general, the optimum operation pH of the system matches to the optimum operation pH of the enzymes responsible for the bioconversion process of the biomass into fermentable sugars. Cellulase, the most used enzymatic complex in the saccharification process of lignocellulosic biomasses, expresses its major activity in the pH range that ranges from 4.5 to 5.5. This pH range, besides favoring the catalytic process, also helps in maintaining the stability of the enzymatic complex for longer time periods, which extends the shelf life of the biocatalyst impacting beneficially and in a crucial manner the final cost of the process.
Conventional buffering solutions such as sodium citrate and sodium acetate are very expensive and can also make the productive process impossible to be done in certain situations. Acids and/or bases used for the pH control during the process despite presenting a significantly lower cost in relation to before mentioned solutions still represent a significant portion of the final cost of the process when compared to the process using stillage as the buffering agent. Thus, it the use of effective and cheap buffering agents becomes extremely desirable in the aforementioned process.
The use of stillage in the saccharification process of lignocellulosic biomasses presents many advantages when compared to conventional processes, but certainly an advantage of great importance is the significant savings on water consumption in the step of enzymatic hydrolysis of biomasses (pretreated or not), once the stillage can also substitute all necessary water in this specific process.
The presence of stillage in the enzymatic hydrolysis process of lignocellulosic biomasses allows the formation of chemical compounds which have the ability to promote the buffering effect of the reaction medium, that is, to maintain the pH inside a specific desirable range in order to provide a favorable environment to the suitable functioning of the enzymes making part of the enzymatic complex, which need well defined conditions to perform the breaking of bonds of their specific substrates, in order to maximize the generation of fermentable sugars from the lignocellulosic biomass used.
In the buffering process of the reaction medium, salts present in the stillage such as, for example, sodium, match to acids generated during the pretreatment process of the biomass, such as, for example, acetic acid, forming chemical compounds, such as for example, sodium acetate, which directly acts on the maintenance of the medium pH in certain ranges. Hence, the buffering effect arises from the chemical reaction which takes place between compounds naturally present in the stillage and in the pretreated biomass, dispensing thus the advance preparation of the buffering solution.
The present invention has as main advantages:
In the patent scope, some relevant documents have been identified, which will be discussed hereinafter.
The document U.S. Pat. No. 7,807,419 discloses a process for saccharification of pretreated biomass in order to obtain high concentrations of fermentable sugars. Specifically, it is addressed to a process using a batch wise feeding system having a reduction in the size of particles. The present invention differs from this document by comprising the use of the stillage as the buffering agent of the saccharification reaction of biomasses, as well as the additive to fermentation due to the nitrogen content present in its composition.
The document US 2010/0086981 presents compositions and methods to improve the saccharification of biomasses with enzymes and modified microorganisms. Said document mentions the use of sodium citrate during the reaction. The present invention differs from this document by dispensing the use of sodium citrate, substituting it by the available stillage in large volumes in the sugar cane mills.
The document US 2010/0159515 describes a method of pretreatment of lignocellulosic biomasses mentioning the use of a buffer from citrates. The present invention differs from this document by using compounds present in the available stillage in the alcohol and sugar mills or independent distilleries to promote the buffering effect to the reaction medium.
The document WO 2008/040358 describes the use of a fermentation byproduct, the stillage, which is rich in potassium as the fertilizing agent. This document also says that the stillage rich in potassium is poor in amino acids and proteins, since the same have already been removed in previous steps. The present invention differs from this document by previewing the use of the stillage resulting from the industrial alcohol fermentation rich in nitrogen (to 1 g/L) not as the fertilizing agent, but as the buffering agent of the saccharification process of lignocellulosic biomasses; in addition, this stillage also shows itself suitable to the step of alcoholic fermentation, since it represents an additional source of nitrogen, essential macro nutrient to said fermentation process.
The document EP 048061 describes a process for recycling the stillage comprising the steps of concentration and burning of the stillage. However, nothing is said about its use in hydrolytic (acids or enzymatic) and/or fermentation processes; neither is about its characteristics as buffering agent or source of nitrogen.
The document WO 2008/116278 describes the stillage recycling as additive in animal feed, the stillage passing through a process of distillation and concentration, followed by dehydration.
The document EP 769915 describes the use of organic acids derived from the stillage; such compounds prove especially useful in microbial crops.
The present invention differs from this and from the other documents by using the stillage (or any residue/byproduct derived from the fermented wine distillation process) in any state of treatment (raw, filtered, concentrated, etc) as buffering agent of saccharification processes of lignocellulosic biomasses and fermentation additive (additional source of nitrogen).
What is known from the literature is that no documents were found previewing or suggesting the teachings of the present invention, in such a way that the solution proposed here is new and has inventive activity in relation to the state of the art.
The present invention describes the use of the stillage as the buffering agent of the saccharification processes of lignocellulosic biomasses and the additional source of nitrogen in fermentation processes, regardless of the source and the form in which such biomasses have been produced. In summary, the present invention has as the main competitive advantages the high efficiency, low cost and the preservation of the environment.
An object of the present invention is a saccharification process of lignocellulosic biomasses comprising the addition of the stillage (or any residue/byproduct derived from the process of fermented wine distillation) as the buffering agent to the reaction medium.
In a preferred embodiment, the enzymatic hydrolysis process is a saccharification process and it can occur under any selected configuration from the group comprising SHF (Separated Enzymatic hydrolysis and Fermentation), SSF(Simultaneous Enzymatic hydrolysis and Fermentation), SSCF (Enzymatic hydrolysis, Simultaneous Fermentation and Co-fermentation), CBP (Enzyme Production, Simultaneous Enzymatic hydrolysis and Fermentation), SEPHY (Enzyme Production and Enzymatic hydrolysis separated from the Fermentation) and combinations thereof.
It is a further object of the invention to provide a buffering agent made of stillage, which is useful in enzymatic hydrolysis processes.
It is a further object of the invention to provide the use of stillage as the buffering agent, comprising the step of collecting the stillage from the distillation process of wine resulting from the alcoholic fermentation process.
In another aspect, the present invention provides a fermentation process comprising the addition of a fermentation additive which is rich in nitrogen and essential to the fermentation process in question.
It is a further object of the present invention to provide a fermentation process comprising a step of fermentation in the presence of a fermentation additive made of stillage.
It is a further object of the present invention to provide an ethanol production process comprising the fermentation of sugars in the presence of a fermentation additive made of stillage.
It is a further object of the present invention to provide a fermentation additive made of stillage, which is useful as the source of nitrogen.
It is a further object of the present invention to provide a process of preparing fermentation additive comprising the step of collecting the stillage from the distillation process of wine resulting from the alcoholic fermentation process
These and other objects of the invention will be immediately understood by those skilled in the art and by companies being interested in the segment and will be described in enough details for its reproduction in the description hereinafter.
Examples shown here are only intended to exemplify some of the many ways to carry out the invention without limiting the scope thereof.
Lignocellulosic Vegetal Biomass
The expression lignocellulosic vegetal biomass comprises any type of plant, that is: herbaceous biomass; cultivars such as plants C4—from genera Lolium, Spartina, Panicum, Miscanthus, and combinations thereof; sugar cane bagasse (from the mill and/or diffuser); sugar cane straw; cereal straw such as wheat, rice, rye, barley, oat, maize and the similar (e.g. switchgrass); wood, trunks and sticks of banana trees; cactuses and combinations thereof. In addition, lignocellulosic materials can also comprise cardboard, sawdust, newspaper and agroindustrial or municipal waste and the similar.
Vegetal biomasses from different origins can present particular differences, although they own a relatively similar global chemical composition. Some variations in the composition among different species and inside the same species are due to the environmental and genetic variabilities, despite the localization of the vegetal tissue in different parts of the plant. Typically, lignocellulosic biomasses present from 35% to 50% of cellulose, from 20% to 35% of hemicellulose and from 20% to 30% of lignin. In addition to these majority fractions, there are still minority amounts of ashes, phenolic compounds, organic acids and compounds called extractives. Cellulose and hemicelluloses of the vegetal tissue are constituted by structural carbohydrates (e.g. glycans, xylans, manans) and they are in general called saccharide fraction. Lignin, on the other hand, represents the phenolic fraction of the vegetal biomass.
Stillage
In the present invention, it is understood as stillage any residue from the distillation process of wine without yeasts, obtained after fermentation and separation of yeast cells, generally by centrifugation, but not limited to it.
Buffering Agent
In chemistry, buffer solutions are solutions that can mitigate variations in pH, stabilizing it at a relatively constant value, even if the system suffers disruption by adding acids or bases.
The stillage obtained in the present invention, for its high concentration of ions such as sodium, is able to react with the acids generated in the pretreatment process/hydrolysis, then maintaining the pH of the medium in a constant range and favorable for enzyme activity.
The stillage of the present invention is very useful in enzymatic hydrolysis processes in general, but specially in saccharification reactions of lignocellulosic biomasses.
The stillage of the present invention, being a byproduct of fermentation, presents low cost and replaces commonly used quite efficiently buffering agents having low cost such as, for example, citric acid.
The buffering agent is produced by a process comprising the step of collecting a stillage produced in the distillation process of wine without yeasts, resulting from the alcoholic fermentation process, and, optionally, filtering, evaporating and/or concentrating it.
Enzymatic Hydrolysis Process
The enzymatic hydrolysis process of the present invention is a process comprising the addition of any amount of stillage to the reaction medium in order to provide its buffering.
In a preferred embodiment, the hydrolysis process is a saccharification process and can occur under any configuration known by the state of the art, and selected from the group comprising SHF (separated Enzymatic hydrolysis and Fermentation), SSF (Simultaneous Enzymatic hydrolysis and Fermentation), SSCF (Simultaneous Enzymatic hydrolysis, Simultaneous Fermentation and Co-Fermentation), CBP (Enzyme production, Enzymatic hydrolysis and Simultaneous Fermentation), SEPHY (Enzyme production and Enzymatic hydrolysis separated from the Fermentation) and combinations thereof.
Fermentation Additive
The fermentation additive of the present invention is a solution rich in nitrogen, essential nutrient for growing microorganisms responsible for the fermentation, even if they are yeasts or bacteria.
The stillage obtained in the present invention, for its high concentration of nitrogen, serves as an additional nutritional source in the fermentation process. Thus, the stillage of the present invention is very useful in the fermentation process in general and in special in alcoholic fermentation reactions.
The fermentation additive is produced by a process comprising the step of collecting a stillage produced in the distillation process of wine without yeasts, resulting from the alcoholic fermentation process, and, optionally, filtering, evaporating and/or concentrating it.
Fermentation Process
The fermentation process of the present invention encompasses any fermentation process, whether bacterial or by means of yeasts, comprising a step of fermentation in the presence of a fermentation additive made of stillage.
In a preferred embodiment, the fermentation process of the present invention aims to obtain ethanol.
Materials and Methods
Lignocellulosic Material: Bagasse typical of sugar cane (humidity of approximately 50%) was collected in an alcohol and sugar mill and located in Piracicaba/SP, immediately after sugar cane milling (fresh bagasse).
Pretreatment with Steam explosion: Sugarcane bagasse “in natura” was pretreated with vapor (Steam Explosion) aiming to promote chemical and structural changes in the biomass, aiming to obtain a substrate (pulp) having a high cellulose content and high accessibility of the matrix Lignin-carbohydrate to cellulolytic enzymes. In this sense, effective processes are characterized by high removal of hemicelluloses and selective extraction of xylose (monomer and oligomer), having minimal glucose removal. Furthermore, such processes must produce minimum of compounds inhibiting enzymatic action (e.g. furfural, HMF, humic acids and phenolic derivatives), produced from the breakdown of carbohydrates and of lignin.
Pretreatment experiments with vapor were performed in the offices of CTC (Sugarcane Research Center, Piracicaba/SP) and, in general, in a single step. In
Characterization of Pretreated bagasse: Sugar cane bagasse “in natura” and pretreated with steam explosion were characterized for its main constituents (structural carbohydrates and lignin), following the experimental methodology based on the protocol designed by National Renewable Energy Laboratories (NREL), United States of America (Sluiter et. al., 2004).
The characterization of these materials requires the determination of the humidity content, using differential gravimetry in electronic scale after greenhouse for measuring the percentage in relation to the dry base of the material. For the determination of insoluble lignin content in acid and structural carbohydrates a sample of dry bagasse was mixed to H2SO4 (72%), under agitation for 1 hour. The reaction was stopped by the addition of distilled water. Next, for the complete hydrolysis of the remaining oligomers, the suspension was autoclaved (121° C.) for 1 hour. The liquid fraction (hydrolysate) was used for determining structural carbohydrates by liquid chromatography (HPLC) and the solid fraction was washed with distilled water and dried in greenhouse (105° C.) for subsequent calcination (575° C.) and determination of lignin by gravimetry.
The determination of structural carbohydrates by HPLC was done using the refractive index detector (IR), using external patterns for each component, column Aminex HPX 87H (300×7.8 mm, BIO-RAD) and mobile phase 5 mM H2SO4 having a flow rate of 0.6 mL/min at 45° C.
Enzymatic hydrolysis: Pretreated sugarcane bagasse was subjected to enzymatic hydrolysis using different concentrations of industrial stillage which was typical in the reaction medium, according to Table 1 below. In parallel, experiments in the absence of stillage, herein called reference experiments, were also performed under identical experimental conditions:
TABLE 1
Enzymatic hydrolysis
Experiment
Relation % Stillage/% Water
1
10%-90%
2
20%-80%
3
30%-70%
4
40%-60%
5
50%-50%
6
60%-40%
7
70%-30%
8
80%-20%
9
90%-10%
10
100%-0%
The experiments of enzymatic hydrolysis were performed in a 60 L-reactor, under the following experiment conditions: 50° C.; pH 4.8-5.2; 8% of total solids; the enzyme load of 13.5 mL of enzyme/kg of dried bagasse and 48 hours of reaction. The reactions of hydrolysis were conducted using the enzyme Cellic Ctec 2, given by Novozymes® (Novozymes Latin America Ltda.—Araucaria/PR, Brazil). The conversion of cellulose present in the biomass in glucose (fermentable sugar) reached in each test conducted was calculated by the following equation (1):
wherein: MExperimental glucose is the glucose mass present in the hydrolysate broth after 48 hours of reaction; Mblank is the glucose mass measured in the essay performed under identical experimental conditions, but in the absence of enzymes; MCellulose is the initial mass of cellulose present in the pretreated bagasse and 1,111 is the conversion factor from cellulose to glucose.
Pretreated bagasse Composition: The bagasse composition pretreated with steam explosion was determined using the experimental methodology based on the procedure designed by NREL, as previously described, and it is shown in Table 2 as follows:
TABLE 2
Bagasse Composition pretreated with steam explosion (dry
base) in relation to its majorities fractions.
Pretreated bagasse
Percentage in dry base
Humidity
65.42%
Dry solids
34.58%
Cellulose
59.20%
Hemicellulose
2.80%
Lignin
33.30%
Soluble solids
17.50%
Insoluble solids
82.50%
As it can be seen in the above table, the treatment with vapor preserved the cellulose and lignin fractions and significantly solubilized a hemicellulose, as desired. Thus, it is expected that the accessibility of the enzymes to their specific substrates become considerably easier in the pretreated bagasse.
Enzymatic hydrolysis of cellulose having solids load of 8%: In all experiments performed in the presence of stillage, the final set of reactional suspension pH was done with sodium hydroxide (NaOH). Experiments with hydrolysis in the absence of stillage and the so called here “reference” were performed in triplicate, using buffer solutions sodium citrate 50 mM, pH 5.
As it can be observed in
Those skilled in the art will value the teachings presented here and they will be able to reproduce the invention in the presented embodiments and in other variants, within the scope of the appended claims.
Tome, Jose Augusto Travassos Rios, Neto, Oswaldo Godoy, Galvao, Celia Maria Araujo, Andrade, Liliane Pires, Teodoro, Juliana Conceicao
| Patent | Priority | Assignee | Title |
| Patent | Priority | Assignee | Title |
| 5914040, | Feb 01 1994 | Rhone-Poulenc Chimie | Process for the purification of a medium containing organic waste |
| 7807419, | Aug 22 2007 | SUSTAINABLE TECHNOLOGY CORPORATION | Process for concentrated biomass saccharification |
| 20050136520, | |||
| 20100086981, | |||
| 20100159515, | |||
| 20110262984, | |||
| CN101838673, | |||
| EP190610, | |||
| EP48061, | |||
| EP769915, | |||
| FR2697266, | |||
| RU2102480, | |||
| RU2208630, | |||
| WO2008040358, | |||
| WO2008116278, | |||
| WO2009155673, | |||
| WO2010100224, |
| Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
| Mar 05 2012 | CTC-Centro de Tecnologia Canavieira S.A. | (assignment on the face of the patent) | / | |||
| Sep 30 2013 | GALVAO, CELIA MARIA ARAUJO | CTC-CENTRO DE TECNOLOGIA CANAVIEIRA S A | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 031438 | /0217 | |
| Sep 30 2013 | TEODORO, JULIANA CONCEICAO | CTC-CENTRO DE TECNOLOGIA CANAVIEIRA S A | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 031438 | /0217 | |
| Sep 30 2013 | ANDRADE, LILIANE PIRES | CTC-CENTRO DE TECNOLOGIA CANAVIEIRA S A | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 031438 | /0217 | |
| Sep 30 2013 | TOME, JOSE AUGUSTO TRAVASSOS RIOS | CTC-CENTRO DE TECNOLOGIA CANAVIEIRA S A | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 031438 | /0217 | |
| Sep 30 2013 | NETO, OSWALDO GODOY | CTC-CENTRO DE TECNOLOGIA CANAVIEIRA S A | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 031438 | /0217 |
| Date | Maintenance Fee Events |
| Sep 02 2020 | M1551: Payment of Maintenance Fee, 4th Year, Large Entity. |
| Jul 17 2024 | M1552: Payment of Maintenance Fee, 8th Year, Large Entity. |
| Date | Maintenance Schedule |
| Apr 04 2020 | 4 years fee payment window open |
| Oct 04 2020 | 6 months grace period start (w surcharge) |
| Apr 04 2021 | patent expiry (for year 4) |
| Apr 04 2023 | 2 years to revive unintentionally abandoned end. (for year 4) |
| Apr 04 2024 | 8 years fee payment window open |
| Oct 04 2024 | 6 months grace period start (w surcharge) |
| Apr 04 2025 | patent expiry (for year 8) |
| Apr 04 2027 | 2 years to revive unintentionally abandoned end. (for year 8) |
| Apr 04 2028 | 12 years fee payment window open |
| Oct 04 2028 | 6 months grace period start (w surcharge) |
| Apr 04 2029 | patent expiry (for year 12) |
| Apr 04 2031 | 2 years to revive unintentionally abandoned end. (for year 12) |